CN113725519A - Liquid cooling system with dehumidification function - Google Patents
Liquid cooling system with dehumidification function Download PDFInfo
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- CN113725519A CN113725519A CN202111015583.1A CN202111015583A CN113725519A CN 113725519 A CN113725519 A CN 113725519A CN 202111015583 A CN202111015583 A CN 202111015583A CN 113725519 A CN113725519 A CN 113725519A
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- 238000007791 dehumidification Methods 0.000 title claims abstract description 67
- 238000001816 cooling Methods 0.000 title claims abstract description 46
- 239000007788 liquid Substances 0.000 title claims abstract description 45
- 239000003507 refrigerant Substances 0.000 claims abstract description 55
- 238000010438 heat treatment Methods 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- 230000007613 environmental effect Effects 0.000 claims description 24
- 230000008901 benefit Effects 0.000 abstract description 3
- 230000010354 integration Effects 0.000 abstract description 2
- 239000002826 coolant Substances 0.000 description 12
- 230000009471 action Effects 0.000 description 11
- 238000005057 refrigeration Methods 0.000 description 8
- 238000004378 air conditioning Methods 0.000 description 6
- 238000004146 energy storage Methods 0.000 description 6
- 239000000498 cooling water Substances 0.000 description 5
- 239000000110 cooling liquid Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/60—Heating or cooling; Temperature control
- H01M10/61—Types of temperature control
- H01M10/613—Cooling or keeping cold
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/265—Drying gases or vapours by refrigeration (condensation)
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/60—Heating or cooling; Temperature control
- H01M10/61—Types of temperature control
- H01M10/615—Heating or keeping warm
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/60—Heating or cooling; Temperature control
- H01M10/65—Means for temperature control structurally associated with the cells
- H01M10/656—Means for temperature control structurally associated with the cells characterised by the type of heat-exchange fluid
- H01M10/6561—Gases
- H01M10/6563—Gases with forced flow, e.g. by blowers
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/60—Heating or cooling; Temperature control
- H01M10/65—Means for temperature control structurally associated with the cells
- H01M10/656—Means for temperature control structurally associated with the cells characterised by the type of heat-exchange fluid
- H01M10/6567—Liquids
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Air Conditioning Control Device (AREA)
Abstract
The invention relates to a liquid cooling system with a dehumidification function, which comprises a refrigerant main loop unit and a heating and cooling circulation unit, wherein the refrigerant main loop unit comprises a compressor, a first heat exchanger, a throttle valve and a second heat exchanger which are sequentially and circularly connected, the liquid cooling system comprises a dehumidification unit, and the dehumidification unit is used as a branch of the refrigerant main loop unit and is respectively connected with an outlet of the throttle valve and an inlet of the compressor. The invention has the comprehensive advantages of high system integration level, high overall energy efficiency, flexible system configuration and low cost.
Description
Technical Field
The invention relates to the field of new energy storage systems, in particular to a liquid cooling system with a dehumidification function.
Background
The battery system has high density and concentrated heat generation, and if the generated heat cannot be discharged in time, the service life of the battery system can be reduced, and thermal runaway and even explosion can occur. In a low-temperature environment, if the energy storage battery is not heated, the problems of poor charging and discharging performance, accelerated decay of service life, even lithium precipitation and the like of a battery system can occur. The battery system is also easy to corrode and lose efficacy or even cause safety accidents due to the overlarge environmental humidity. Therefore, the environmental control system of the battery system needs to include three functions of cooling, heating, and dehumidifying.
Chinese patent CN111769299A discloses a battery thermal management system with dehumidification function and a dehumidification method. The heat management system is used for cooling, heating or dehumidifying an energy storage battery and comprises a compressor, a first heat exchanger, a second heat exchanger, a third heat exchanger, a fourth heat exchanger and an air driving unit, wherein in a first state, the air driving unit is used for driving air to be dehumidified to sequentially pass through the third heat exchanger and the fourth heat exchanger, and in a second state, the air driving unit is used for driving the air to be dehumidified to sequentially pass through the fourth heat exchanger and the third heat exchanger. In the refrigeration mode of the patent, the refrigerant passing through the heat exchanger is in a low-temperature and low-pressure state; under the driving action of the air driving unit, the dehumidified air in the energy storage battery container is in contact with the heat exchanger, and the carried moisture is condensed and separated out under the heat absorption action of the refrigerant, so that the dehumidification effect is achieved. And then, the dehumidified air is continuously contacted with the fourth heat exchanger, because the cooling water absorbs the heat of the high-temperature high-pressure gaseous refrigerant in the heat exchanger, the cooling water after absorbing the heat enters the heat exchanger to be converted into an air heater, and the dehumidified air is returned to the temperature under the action of the cooling water. The processes are circulated, and the refrigeration and dehumidification functions are achieved. In the heating mode, a part of the cooling water with lower temperature from the circulation port of the heat exchanger enters the heat exchanger arranged in parallel with the cooling tower. At this time, the heat exchanger serves as a function of dehumidification evaporation. Under the driving action of the air driving unit, the dehumidified air in the energy storage battery container exchanges heat with the heat exchanger, moisture carried by the air is condensed and separated out under the action of low-temperature cooling water, the dehumidification effect is achieved, the dehumidified air is continuously contacted with the heat exchanger, and the air is warmed under the heat release action of a refrigerant of the dehumidified air. The above processes are circulated, so that the heating and dehumidifying functions are achieved. However, this solution has the following drawbacks: (1) the system is complex, and the application range is limited; (2) the added heat exchange loop can reduce the heat efficiency of the system; (3) the complexity of the system is improved and the reliability of the system is reduced due to the addition of the rotating parts; (4) the system has higher difficulty in treating the condensed water; (5) the system cannot be flexibly configured, and a third heat exchanger and a fourth heat exchanger are required to be simultaneously provided.
Therefore, there is a need in the art for a liquid cooling system with dehumidification function that is simple in structure, high in overall energy efficiency, flexible in configuration, and low in cost.
Disclosure of Invention
The present invention is directed to a liquid cooling system with dehumidification function to overcome the above-mentioned drawbacks of the prior art.
In order to achieve the object of the present invention, the present application provides the following technical solutions.
In a first aspect, the application provides a liquid cooling system with dehumidification function, the liquid cooling system includes refrigerant major loop unit and heating cooling circulation unit, wherein, refrigerant major loop unit is including in proper order and circulation connection's compressor, first heat exchanger, choke valve and second heat exchanger, its characterized in that, the liquid cooling system is including the dehumidification unit, the dehumidification unit is as the branch road of refrigerant major loop unit, and respectively with the export of choke valve and the access connection of compressor. In this application, the first heat exchanger is an air-cooled heat exchanger or a plate heat exchanger.
In an embodiment of the first aspect, the dehumidification unit includes a third heat exchanger and a first valve, two ends of the third heat exchanger are respectively connected to the outlet of the throttle valve and the inlet of the compressor, and the first valve is disposed at the inlet or the outlet of the third heat exchanger.
In an embodiment of the first aspect, the throttle valve comprises a first throttle valve, and the inlet of the third heat exchanger is connected to the outlet of the first throttle valve.
In an embodiment of the first aspect, the throttle valve includes a first throttle valve and a second throttle valve arranged in parallel, an inlet of the third heat exchanger is divided into two paths, one path is connected to an outlet of the second throttle valve, a second valve is arranged on a connecting line, the other path is connected to an outlet of the first throttle valve, a first valve is arranged on the connecting line, and an outlet of the third heat exchanger is connected to an inlet of the compressor.
In an embodiment of the first aspect, the dehumidification unit includes a fourth heat exchanger, one end of the fourth heat exchanger is communicated with the outlet of the compressor, and the other end of the fourth heat exchanger is divided into two paths, wherein one path is connected to the inlet of the first throttling valve, and the other path is connected to the inlet of the second throttling valve.
In one embodiment of the first aspect, a third valve is provided in a connection pipeline between the fourth heat exchanger and the first throttle valve inlet; and a fourth valve is arranged on a connecting pipeline between the fourth heat exchanger and the inlet of the second throttling valve.
In an implementation manner of the first aspect, the liquid cooling system is provided with a four-way valve, a first connecting port of the four-way valve is connected with an outlet of the compressor, a second connecting port of the four-way valve is connected with one end of the first heat exchanger, and a third connecting port of the four-way valve is connected with one end of the second heat exchanger; and a fourth connecting port of the four-way valve is connected with an inlet of the compressor.
In one embodiment of the first aspect, the heating and cooling cycle unit includes a second heat exchanger, a heater, a water pump, and a heat exchange plate unit that are connected in a cycle, and a heat source pipeline of the second heat exchanger is connected in the heating and cooling cycle unit.
In one embodiment of the first aspect, a water tank is provided in the heating-cooling circulation unit, and the water tank is provided with a filling opening.
In one embodiment of the first aspect, the dehumidification unit and the heat exchange plate unit are installed within the same or different target environmental control system; and an air driving unit is arranged in the target environmental control system provided with the dehumidification unit and used for driving air in the target environmental control system to circularly flow.
Compared with the prior art, the invention has the beneficial effects that:
the system has the functions of refrigeration, heating and refrigeration and dehumidification, and is particularly suitable for a large-scale new energy storage system; compared with the traditional liquid cooling system (with the refrigeration function and the PTC heating function), the dehumidification function of the system can be realized only by adding one branch, one evaporator and one air driving unit. Therefore, the invention has the comprehensive advantages of high system integration level, high overall energy efficiency, flexible configuration and low cost.
Drawings
FIG. 1 is a schematic diagram of a conventional liquid cooling system;
FIG. 2 is a schematic view showing the construction of a heat pump air conditioning system according to embodiment 1;
FIG. 3 is a schematic structural view of a heat pump air conditioning system according to embodiment 2;
FIG. 4 is a schematic structural diagram of the heat pump air conditioning system in the cooling and dehumidifying mode in embodiment 3;
fig. 5 is a schematic structural diagram of the heat pump air conditioning system in the heating and dehumidifying mode in embodiment 3.
In the drawing, 10 is a compressor, 11 is a first valve, 12 is a second valve, 13 is a third valve, 14 is a fourth valve, 20 is a first heat exchanger, 21 is a first throttle valve, 22 is a second throttle valve, 40 is a second heat exchanger, 31 is a first air driving unit, 32 is a second air driving unit, 51 is a water tank, 52 is a PTC heater, 53 is a water pump, 60 is a fourth heat exchanger, 70 is a four-way valve, 701 is a first connection port, 702 is a second connection port, 703 is a third connection port, 704 is a fourth connection port, 81 is a target environmental control system, 80# N is a heat exchange plate unit, 90 is a third heat exchanger, and 100 is a dehumidification tank.
Detailed Description
Unless otherwise defined, technical or scientific terms used herein in the specification and claims should have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. All numerical values recited herein as between the lowest value and the highest value are intended to mean all values between the lowest value and the highest value in increments of one unit when there is more than two units difference between the lowest value and the highest value.
In the following detailed description of the embodiments of the present invention, reference is made to the accompanying drawings, where it is noted that in the interest of brevity and conciseness, not all features of an actual embodiment may be described in detail in this specification. Modifications and substitutions to the embodiments of the present invention may be made by those skilled in the art without departing from the spirit and scope of the present invention, and the resulting embodiments are within the scope of the present invention.
The conventional liquid cooling system structure is shown in fig. 1, and includes the following components: the air-conditioning system includes a compressor 10, a first heat exchanger 20, a first throttle valve 21, a second heat exchanger 40, a water tank 51, a PTC heater 52, a water pump 53, a heat exchange plate unit 80# N (including a heat exchange plate unit 80#1, heat exchange plate units 80#2, …, and a heat exchange plate unit 80# N), a target environmental control system 81 (such as a battery box, etc.), and a first air driving unit 31.
The compressor 10 is provided with a refrigerant inlet and a refrigerant outlet, the first heat exchanger 20 is provided with a first circulation port and a second circulation port, the second heat exchanger 40 is provided with a first circulation port, a second circulation port, a third circulation port and a fourth circulation port, and refrigerant is communicated between the first circulation port and the second circulation port of the second heat exchanger 40 to be used as a cold source pipeline of the second heat exchanger 40; a high-temperature refrigerant is passed between the third flow port and the fourth flow port as a heat source line. A refrigerant outlet of the compressor 10 is connected to a first flow port of the first heat exchanger 20, a second flow port of the first heat exchanger 20 is communicated with an inlet of the first throttle valve 21, an outlet of the first throttle valve 21 is connected to a first flow port of the second heat exchanger 40, and a second flow port of the second heat exchanger 40 is connected to a refrigerant inlet of the compressor 10. The fourth circulation port of the second heat exchanger 40 is sequentially connected to the water tank 51, the PTC heater 52 and the water pump 53, and then connected to the heat exchange plate unit 80# N, and finally circularly connected to the third circulation port of the second heat exchanger 40.
The traditional liquid cooling system cannot realize dehumidification management of the target environmental control system 81, so that the problem that a large amount of condensed water is generated inside the target environmental control system 81 due to high system humidity of an actual system, and potential safety hazards are generated on high-voltage electric devices.
Examples
The following detailed description will be made with reference to the accompanying drawings, which are provided for the purpose of illustrating the present invention and are intended to provide a detailed description and a specific operation process, but the scope of the present invention is not limited to the following embodiments.
Example 1
A liquid cooling system with dehumidification function is shown in FIG. 2, and comprises the following components: the air conditioner includes a compressor 10, a first heat exchanger 20, a first throttle valve 21, a second heat exchanger 40, a water tank 51, a PTC heater 52, a water pump 53, a heat exchange plate unit 80# N (including a heat exchange plate unit 80#1, heat exchange plate units 80#2, …, heat exchange plate unit 80# N), a target environmental control system 81 (such as a battery box, etc.), a first air driving unit 31, a dehumidification tank 100, a third heat exchanger 90, and a second air driving unit 32.
The compressor 10 is provided with a refrigerant inlet and a refrigerant outlet, the first heat exchanger 20 is provided with a first circulation port and a second circulation port, the second heat exchanger 40 is provided with a first circulation port, a second circulation port, a third circulation port and a fourth circulation port, and cooling liquid is communicated between the first circulation port and the second circulation port of the second heat exchanger 40 to be used as a cold source pipeline of the second heat exchanger 40; high-temperature coolant is introduced between the third flow port and the fourth flow port as a heat source line. A refrigerant outlet of the compressor 10 is connected to a first flow port of the first heat exchanger 20, a second flow port of the first heat exchanger 20 is communicated with an inlet of the first throttle valve 21, an outlet of the first throttle valve 21 is connected to a first flow port of the second heat exchanger 40, and a second flow port of the second heat exchanger 40 is connected to a refrigerant inlet of the compressor 10. The fourth circulation port of the second heat exchanger 40 is sequentially connected to the water tank 51, the PTC heater 52 and the water pump 53, and then connected to the heat exchange plate unit 80# N, and finally circularly connected to the third circulation port of the second heat exchanger 40. The dehumidification tank 100 is disposed in the target environmental control system 81, and a third heat exchanger 90 and a second air driving unit 32 are disposed in the dehumidification tank 100, one end of the third heat exchanger 90 is connected to an outlet of the first throttle valve 21, and the other end of the third heat exchanger 90 is connected to a refrigerant inlet of the compressor 10. The second air driving unit 32 can drive the air in the target environmental control system 81 to circulate.
The working principle of the system is as follows:
main refrigerant circuit: compressor 10 → first heat exchanger 20 → throttle valve 21 → second heat exchanger 40 → compressor 10;
a refrigerant dehumidification circuit: compressor 10 → first heat exchanger 20 → throttle valve 21 → third heat exchanger 90 → compressor 10;
cooling liquid loop: the water pump 53 → the heat exchange plate unit 80# N → the second heat exchanger 40 → the water tank 51 → the PTC heater 52 → the water pump 53.
(1) A refrigeration function:
the refrigerant is compressed to a high-temperature high-pressure gas state by the compressor 10, enters the first heat exchanger 20, exchanges heat with cold air blown out by the first air driving unit 31, is converted into a low-temperature high-pressure liquid state, and further is converted into a low-temperature low-pressure gas-liquid mixed state by the throttle valve 21. The low-temperature and low-pressure refrigerant enters the second heat exchanger 40 and exchanges heat with the coolant in the coolant circuit, so that the target environment control system 81 is cooled.
(2) The dehumidification function is as follows:
the cold energy of the evaporator of the dehumidification loop is led out from the main loop of the refrigerant, specifically, the low-temperature and low-pressure refrigerant passing through the throttle valve 21 flows into the third heat exchanger 90, at this time, under the action of the air driving unit 32, the water vapor in the environment of the target environmental control system 81 is condensed after passing through the third heat exchanger 90 and collected in the dehumidification box 100, and the dehumidification effect on the target environmental control system 81 is further realized.
(3) The heating function is as follows:
in the heating function, the refrigerant main circuit is in a standby state, and the PTC heater 52 heats the coolant circuit, thereby achieving a heating effect on the target environmental control system 81.
Example 2
A liquid cooling system with dehumidification function, the structure of which is shown in fig. 3, is substantially the same as that of embodiment 1, except that: a first valve 11 is provided at the inlet of the third heat exchanger 90.
The target environmental control system 81 itself has a certain IP level, and therefore, in actual use, it is not necessary to perform real-time dehumidification, and the humidity of the system can be maintained for a certain period of time by once dehumidification. In turn, compared with embodiment 1, by adding the first valve 11, the opening time of dehumidification can be controlled by the first valve 11, and the energy efficiency of the system can be further improved.
Example 3
A liquid cooling system with dehumidification function is shown in fig. 4 and 5, and comprises the following components:
the air dehumidifying apparatus includes a compressor 10, a four-way valve 70, a first heat exchanger 20, a first throttle valve 21, a second throttle valve 22, a second heat exchanger 40, a water tank 51, a PTC heater 52, a water pump 53, heat exchange plate units 80#2, …, a heat exchange plate unit 80# N, a target environmental control system 81 (such as a battery box, etc.), a first valve 11, a second valve 12, a third valve 13, a fourth valve 14, a third heat exchanger 90, a fourth heat exchanger 60, a first air driving unit 31, an air driving unit 32, and a dehumidifying tank 100.
An outlet of the compressor 10 is connected to a first connection port 701 of the four-way valve 70, a second connection port 702 of the four-way valve 70 is connected to one end of the first heat exchanger 20, the other end of the first heat exchanger 20 is divided into three paths, the first path is connected to one end of the first throttle valve 21, and the second path is connected to one end of the second throttle valve 22.
One end of the first throttle valve 21 is divided into two paths, one path is connected to the first heat exchanger 20, the other path is connected to one end of the third heat exchanger 90, and a first valve 11 is disposed on the connecting path. The other end of the first throttle valve 21 is also divided into two paths, the first path is connected with one end of the cold source pipeline of the second heat exchanger 40, the other path is connected with one end of the fourth heat exchanger 60, and the third valve 13 is arranged on the connecting pipeline.
One end of the second throttle valve 22 is divided into two paths, the first path is connected to the first heat exchanger 20, the other path is connected to one end of the fourth heat exchanger 60, the fourth valve 14 is disposed on the connection pipeline, the other end of the second throttle valve 22 is also divided into two paths, the first path is connected to one end of the cold source pipeline of the second heat exchanger 40, the other path is connected to one end of the third heat exchanger 90, and the second valve 12 is disposed on the connection pipeline.
The other end of the cold source line of the second heat exchanger 40 is connected to the third connection port 703 of the four-way valve 70, and the fourth connection port 704 of the four-way valve 70 is connected to the inlet of the compressor 10. The heat source pipeline of the second heat exchanger 40 is sequentially and circularly connected with the water tank 51, the PTC heater 52, the water pump 53 and the heat exchange plate unit 80# N.
The other end of the third heat exchanger 90 is connected to the inlet of the compressor 10.
One end of the fourth heat exchanger 60 is connected with the outlet of the compressor 10, the other end of the fourth heat exchanger 60 is divided into two paths, the first path is connected with one end of the first throttle valve 21, and a third valve 13 is arranged on the connecting path; the other is connected to one end of a second throttle 22, and a fourth valve 14 is provided in the connection line.
In the present embodiment, the third heat exchanger 90 and the fourth heat exchanger 60 are both disposed in the dehumidification tank 100, and the dehumidification tank 100 is further provided with an air driving unit 32, and the air driving unit 32 is used for driving the air in the target environmental control system 81 to circularly flow. The first heat exchanger 20 is provided with a first air drive unit 31 for cooling the coolant in the first heat exchanger 20.
The heat pump air conditioning system of the embodiment has two modes, namely a cooling dehumidification mode and a heating dehumidification mode, and the structures are respectively shown in fig. 4 and fig. 5, and the specific principle is as follows:
a refrigeration dehumidification mode:
valve state: the first valve 11 is closed, the second valve 12 is opened, the third valve 13 is closed, and the fourth valve 14 is opened.
Main refrigerant circuit: compressor 10 → first connection port 701 of the four-way valve 70 → second connection port 702 of the four-way valve 70 → first heat exchanger 20 → second throttle valve 22 → second heat exchanger 40 → third connection port 703 of the four-way valve 70 → fourth connection port 704 of the four-way valve 70 → compressor 10.
Refrigerant dehumidification evaporator circuit: compressor 10 → first connection port 701 of four-way valve 70 → second connection port 702 of four-way valve 70 → first heat exchanger 20 → second throttle valve 22 → second valve 12 → third heat exchanger 90 → compressor 10.
Refrigerant dehumidification condenser loop: compressor 10 → fourth heat exchanger 60 → fourth valve 14 → second throttle valve 22 → second heat exchanger 40 → third connection port 703 of the four-way valve 70 → fourth connection port 704 of the four-way valve 70 → compressor 10.
Cooling liquid loop: the water pump 53 → the heat exchange plate unit 80# N → the second heat exchanger 40 → the water tank 51 → the PTC heater 52 → the water pump 53.
The working principle of the refrigeration and dehumidification mode is as follows:
the refrigerant is compressed by the compressor 10 into a high-temperature high-pressure gas state, enters the four-way valve 70 through the first connection port 701, passes through the second connection port 702, enters the first heat exchanger 20, exchanges heat with air brought by the first air driving unit 31, is converted into a low-temperature high-pressure liquid state, and further passes through the second throttle valve 22 to be converted into a low-temperature low-pressure gas-liquid mixed state. The low-temperature and low-pressure refrigerant enters the second heat exchanger 40, exchanges heat with the coolant in the coolant circuit to cool the target environmental control system 81, changes the coolant into a low-temperature and low-pressure gas, enters the four-way valve 70 through the third connection port 703, flows out through the fourth connection port 704, and returns to the compressor 10. The above steps are repeated in a circulating way, and the target environment control system is cooled.
The working principle of the dehumidification evaporator is as follows:
the refrigerant is compressed by the compressor 10 into a high-temperature high-pressure gas state, enters the four-way valve 70 through the first connection port 701, passes through the second connection port 702, enters the first heat exchanger 20, exchanges heat with air brought by the first air driving unit 31, is converted into a low-temperature high-pressure liquid state, and further passes through the second throttle valve 22 to be converted into a low-temperature low-pressure gas-liquid mixed state. The low-temperature low-pressure refrigerant enters the third heat exchanger 90 through the second valve 12 to form the cold end of the dehumidifier, under the action of the air driving unit 32, moisture in the air is condensed at the third heat exchanger 90, and the refrigerant is changed into a low-temperature low-pressure gaseous state and flows out of the third heat exchanger 90 to return to the compressor. The humidity control of the third heat exchanger is realized by the circulation reciprocating.
The working principle of the dehumidifying condenser is as follows:
the refrigerant is compressed to a high-temperature high-pressure gaseous state by the compressor 10, part of the high-temperature high-pressure gaseous refrigerant directly enters the fourth heat exchanger 60, and under the action of the air driving unit 32, the cold air passing through the third heat exchanger 90 is heated, at this time, the refrigerant in the fourth heat exchanger 60 is cooled, and then passes through the fourth valve 14 and the second throttle valve 22 in sequence, and is changed into a low-temperature low-pressure gas-liquid mixed state. The low-temperature and low-pressure refrigerant enters the second heat exchanger 40, then enters the four-way valve 70 through the third connection port 703, flows out through the fourth connection port 704, and returns to the compressor 10. The air is heated after being condensed by the circulation reciprocating.
Heating and dehumidifying mode:
valve state: the first valve 11 is open, the second valve 12 is closed, the third valve 13 is open and the fourth valve 14 is closed.
Main refrigerant circuit: compressor 10 → first connection port 701 of the four-way valve 70 → third connection port 703 of the four-way valve 70 → second heat exchanger 40 → first throttle valve 21 → first heat exchanger 20 → second connection port 702 of the four-way valve 70 → fourth connection port 704 of the four-way valve 70 → compressor 10.
Refrigerant dehumidification evaporator circuit: compressor 10 → first connection port 701 of the four-way valve 70 → third connection port 703 of the four-way valve 70 → second heat exchanger 20 → first throttle valve 21 → first valve 61 → third heat exchanger 90 → compressor 10.
Refrigerant dehumidification condenser loop: compressor 10 → fourth heat exchanger 60 → third valve 13 → first throttle valve 21 → first heat exchanger 20 → second connection port 702 of the four-way valve 70 → fourth connection port 704 of the four-way valve 70 → compressor 10.
Cooling liquid loop: the water pump 53 → the heat exchange plate unit 80# N → the second heat exchanger 40 → the water tank 51 → the PTC heater 52 → the water pump 53.
The working principle of the heating and dehumidifying mode is as follows:
the refrigerant is compressed to a high-temperature high-pressure gas state by the compressor 10, enters the four-way valve 70 through the first connecting port 701, enters the second heat exchanger 40 through the third connecting port 703, exchanges heat with the coolant in the coolant loop to heat the target environment control system 81, is changed into a high-pressure low-temperature liquid state after being cooled, flows out of the second heat exchanger 40, enters the first throttle valve 21, and is changed into a low-temperature low-pressure gas-liquid mixed state. The low-temperature and low-pressure refrigerant enters the first heat exchanger 20, exchanges heat with air brought by the first air driving unit 31 to absorb heat from the loop temperature, changes into a low-temperature and low-pressure gaseous state, enters the four-way valve 70 through the second connection port 702, flows out through the fourth connection port 704, and returns to the compressor 10. The above-described operation is repeated cyclically to heat the target environmental control system 81.
The working principle of the dehumidification evaporator is as follows:
the refrigerant is compressed to a high-temperature high-pressure gas state by the compressor 10, enters the four-way valve 70 through the first connecting port 701, enters the second heat exchanger 40 through the third connecting port 703, exchanges heat with the coolant in the coolant loop to heat the target environment control system 81, is changed into a high-pressure low-temperature liquid state after being cooled, flows out of the second heat exchanger 40, enters the first throttle valve 21, and is changed into a low-temperature low-pressure gas-liquid mixed state. Part of the low-temperature and low-pressure refrigerant enters the third heat exchanger 90 after passing through the first valve 11 to form the cold end of the dehumidifier, under the action of the air driving unit 32, moisture in the air in the target environmental control system 81 is condensed at the third heat exchanger 90, and the refrigerant flows out of the third heat exchanger 90 and then returns to the compressor. The circulation is repeated in this way, and the temperature control of the third heat exchanger is realized.
The working principle of the dehumidifying condenser is as follows:
the refrigerant is compressed to a high-temperature high-pressure gaseous state by the compressor 10, part of the high-temperature high-pressure gaseous refrigerant directly enters the fourth heat exchanger 60, and the air passing through the third heat exchanger 90 is heated under the action of the air driving unit 32, at this time, the refrigerant in the fourth heat exchanger 60 is cooled to become a high-pressure low-temperature liquid state, and then the high-pressure low-pressure liquid state is changed to a low-temperature low-pressure gas-liquid mixed state through the third valve 13 and the first throttle valve 21 in sequence. The low-temperature and low-pressure refrigerant enters the first heat exchanger 20, exchanges heat with air brought by the first air driving unit 31 to absorb heat from the loop temperature, enters the four-way valve 70 through the second connection port 702, flows out through the fourth connection port 704, and returns to the compressor 10. The air is heated after being condensed by the circulation reciprocating.
The embodiments described above are intended to facilitate the understanding and appreciation of the application by those skilled in the art. It will be readily apparent to those skilled in the art that various modifications to these embodiments may be made, and the generic principles described herein may be applied to other embodiments without the use of the inventive faculty. Therefore, the present application is not limited to the embodiments herein, and those skilled in the art who have the benefit of this disclosure will appreciate that many modifications and variations are possible within the scope of the present application without departing from the scope and spirit of the present application.
Claims (10)
1. The utility model provides a liquid cooling system with dehumidification function, liquid cooling system includes refrigerant main loop unit and heating cooling circulation unit, wherein, refrigerant main loop unit is including compressor, first heat exchanger, choke valve and the second heat exchanger that just circulation connects in proper order, its characterized in that, liquid cooling system is including the dehumidification unit, the dehumidification unit is as the branch road of refrigerant main loop unit, and the entry linkage with the export of choke valve and compressor respectively.
2. The liquid cooling system with dehumidification function as recited in claim 1, wherein said dehumidification unit comprises a third heat exchanger and a first valve, said third heat exchanger is connected to an outlet of said throttle valve and an inlet of said compressor, respectively, and said first valve is disposed at an inlet or an outlet of said third heat exchanger.
3. The liquid cooling system with dehumidification function of claim 2, wherein said throttling valve comprises a first throttling valve, and an inlet of said third heat exchanger is connected to an outlet of said first throttling valve.
4. The liquid cooling system with dehumidification function as recited in claim 2, wherein said throttle valve comprises a first throttle valve and a second throttle valve connected in parallel, an inlet of said third heat exchanger is divided into two paths, one path is connected to an outlet of said second throttle valve, a second valve is provided on a connection line, the other path is connected to an outlet of said first throttle valve, and a first valve is provided on a connection line, and an outlet of said third heat exchanger is connected to an inlet of said compressor.
5. The liquid cooling system with dehumidification function as recited in claim 4, wherein said dehumidification unit comprises a fourth heat exchanger, one end of said fourth heat exchanger is connected to an outlet of said compressor, and the other end of said fourth heat exchanger is divided into two paths, one of which is connected to an inlet of said first throttling valve and the other of which is connected to an inlet of said second throttling valve.
6. The liquid cooling system with dehumidification function as recited in claim 5, wherein a third valve is disposed on a connection pipeline between said fourth heat exchanger and said first throttle inlet; and a fourth valve is arranged on a connecting pipeline between the fourth heat exchanger and the inlet of the second throttling valve.
7. The liquid cooling system with dehumidification function as in claim 5, wherein said liquid cooling system is provided with a four-way valve, a first connection port of said four-way valve is connected to an outlet of said compressor, a second connection port of said four-way valve is connected to one end of said first heat exchanger, and a third connection port of said four-way valve is connected to one end of said second heat exchanger; and a fourth connecting port of the four-way valve is connected with an inlet of the compressor.
8. The liquid cooling system with dehumidification function as set forth in any one of claims 1 to 7, wherein the heating and cooling cycle unit comprises a second heat exchanger, a heater, a water pump and a heat exchange plate unit which are connected in a cycle, and a heat source pipeline of the second heat exchanger is connected in the heating and cooling cycle unit.
9. The liquid cooling system with dehumidification function as in claim 8, wherein said heating and cooling cycle unit has a water tank therein, said water tank having a filling opening.
10. The liquid cooling system with dehumidification function of claim 8, wherein said dehumidification unit and heat exchange plate unit are installed in the same or different target environmental control system;
and an air driving unit is arranged in the target environmental control system provided with the dehumidification unit and used for driving air in the target environmental control system to circularly flow.
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Application publication date: 20211130 |